ML20238F665

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Forwards Response to IE Bulletin 87-01, Thinning of Pipe Walls in Nuclear Power Plants, Including Plant Programs for Monitoring Wall Thickness of Pipes in Condensate,Feedwater, Steam & high-energy Piping Sys Fabricated W/Carbon Steel
ML20238F665
Person / Time
Site: Point Beach  NextEra Energy icon.png
Issue date: 09/10/1987
From: Fay C
WISCONSIN ELECTRIC POWER CO.
To:
NRC OFFICE OF ADMINISTRATION & RESOURCES MANAGEMENT (ARM)
References
CON-NRC-90 IEB-87-001, IEB-87-1, VPNPD-87-386, NUDOCS 8709160269
Download: ML20238F665 (48)


Text

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77 7 mt et WISCONSIN Electnc eowen couesur.

231 W. MICHIGAN,P.O. BOX 2046, MILWAUKEE WI53201 (414)221-2345 .

VPNPD-87-386 NRC-90 September 10, 1987

,- U. S. NUCLEAR REGULATORY COMMISSION Document Control Desk Washington, D. C. 20555 Gentlemen:

DOCKETS 50-266 AND 50-301 RESPONSE TO IE BULLETIN 87-01 j POINT BEACH NUCLEAR PLANT, UNITS 1 AND 2 IE Bulletin 87-01, " Thinning of Pipe Walls in Nuclear Power Plants", dated July 9, 1987, requested licensees to provide information concerning their programs for monitoring the wall thickness of pipes in condensate, feedwater, steam, and connected high-energy piping systems fabricated of carbon steel. The information provided in the attached report is in ,

response to that request.

Wisconsin Electric' agrees that erosion-corrosion of piping systems is a serious matter. Because of this, we have undertaken a substantial inspection program to accurately assess the current existing conditions of our piping systems.

Repairs or replacements of piping components will be accomplished as inspection results and engineering evaluations dictate.

If you have any further questions, do not hesitate to contact us.

Very trul yours

('

C. W. a Vice resident Nuclear Power 87091602h

$DR ADD M oh66 paa Attachment Copies to NRC Regional Administrator, Region III NRC Resident Inspector Subscribed and sworn to before me this q th- day of September 1987. \

run b Am Notary Public, St'sfe of Wisconsin 4

g My Commission expires S- R7 - 40 . I i

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j DOCKETS 50-266 AND 50-301 {

RESPONSE TO IE BULLETIN 87-01 POINT BEACH NUCLEAR PLANT, UNITS 1 AND'2 Request 1 Identify the codes or standards to which the piping was designed and fabricated.

Response 1 The piping in the balance of plant at Point Beach Nuclear Plant Units 1 and 2  !

were designed and constructed to the requirements of USAS B31.1,1967 edition. I Reguest 2 ,

Describe the scope and extent of your programs for ensuring that pipe wall thicknesses are not reduced below the minimum allowable thickness. Include in j the description the criteria that you have established for:

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a. Selecting noints at which to make thickness measurements

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b. Determining how frequent 1f to make thickness measurements
c. Selecting the methods used to make hickness measurements
d. Making replacement / repair decisions Response 2
a. Selecting Points At Which To Make Wall Thickness Measurements j (1) Philosophy of Exam Point Selection Areas to be inspected for the 1987 Unit I refueling outage were selected based on the consequences of a component failure and the likelihood that service.related degradation was occurring. Using this

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two-fold criteria, a sample of approximately 4% of all possible examination points was looked at. Expansion of the inspection program beyond the original sample size was anticipated had exam q results warrented it. A similar program is planned for the upcoming 1987 Unit 2 refueling / maintenance outage. j l

Systems whose failure could result in significant personnel injury or l equipment damage are considered for inspection. Those syst(ms whose j contained fluid temperature is less than 140 F, or whose pipe  !

diameter is less than, or equal to, 1 inches, are excluded from j inspection without further evaluation. Failure of this category of piping would not have any substantial consequences. Piping systems which do not meet these criteria are evaluated separately for potential inspections.

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ATTACHMENT NES4.CWK.IEB.87-01. RESPONSE Page 2 Points of inspection are selected using a relative " badness factor" and past industry experience. A " badness factor" provides a-

' relative measure of a components susceptibility to service related degradation.

Eacn system to be evaluated is subdivided inte sections based on geometry, pressure, temperature, and flow conditions. Figure A-1 .

.provides a sample of how a typical system is sWodivided. .Each subdivided section is then. evaluated and a relative badness factor for erosion-corrosion is calculated. The badness factor is calculated by a computer program according to the methodology shown in Response 3.

By comparing the relative magnitudes of the erosion-corrosion,  !

badness factors for a given system or piping section, a qualitative l decision can be made as to where the most likely location is for i service related degradation. As the magnitude of a component's badness factor increases, so does its likelihood to experience degradation.

Thereby a method exists for screening potential points for inspection.

Table B-3 is a listing of the exam points selected for the 1987 Unit 1 outage and their associated badness factors.

As an example, suppose the erosion-corrosion badness factors for five points are as follows:

Point E-C Badness Factor A 5 g B 150 l C 20 i D 10 E 1 Point B would be chosen as the most likely candidate for erosion-corrosion to take place whereas Point E would be the least likely. 1 In selecting a sample of exam points for inspection, the piping  !

sections most susceptible to degradation, those points with the  ;

highest badness factors, would be selected for inspection.  !

To qualify the method of selection, an additional random sample equivalent to 56 of the overall sample is taken. In other words, if 1 the original sample size was 100 points, 5 additional points picked l~ randomly, with no regard to their badness factor, are added to the inspection program. In this way a qualitative check of the selection process exists. If service related degradation is noted in this random sample, the selection process would become suspect and further evaluation of the process would be required.

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~ ATTACHMENT IEB 87-01 RESPONSE Page 3 (2) Systems Considered The following systems were considered in the evaluation for potential erosion-corrosion damage:

Main steam Extraction steam Radwaste steam-Turbine exhaust & crossunder steam Feedwater heater and MSR drains & vents Hain feed Condensate Heating steata (3) Points of Inspection There were 3000 areas in Unit 1 evaluated for inspection. Of these 3000 areas, 115 were selected for inspection including a 10% random sample of the original sample for selection qualification purposes.

This amounts to a 4% sample of all the possible points of inspection.

b. Basis For The Frequency of Wall Thickness Measurements The frequency of inspection is based on the proximity of the actual I minimum measured wall thickness to the minimum required wall thickness, as calculated in USAS B31.1, 1967 edition. Proximity to the minimum required wall thickness is determined by establishing a useful remaining life for a given piping component. The predicted useful remaining life (L) is defined as; L= EeSs-tmfg LWR l where, tmjg3= Minimum measured wall thickness in inches for a given piping component, tmjn
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= Required minimum wall thickness in inches as calculated in accordance with USAS B31.1-1967.  !

LWR = Maximum annual local wear rate in inches / year I

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' ATTACHMENT IEB 87-01 RESPONSE

, Page 4 i

The maximum annual wear rate is based on actual changes in wall thickness over a specific period of time. However, for those cases where no previous data exists for a given piping component, wear rate is based on the difference between nominal pipe wall thickness and minimum pipe wall thickness over an assumed 5 year period of time.

Maximum annual local wear rate (LWR) is calculated as follows;

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LWR = $hSs (1)

T LWR = tm n,- tg gr 2)

T where, tnom = Greater of either the standard ASTM nominal wall thickness or the average wall thickness derived from the highest 2 to 3 wall thickness measurements taken during the exam.

T= Time between measurements in years.

If no previous wall thickness measurements exist, assume 5 years.

tggn,= Hinimum measured wall thickness for a given piping component y

at time 1 tmin

= Minimum measured wall thickness taken at the same 2 1 cation as.tg n, but at time 2.

Equation (1) is used when data does not exist from a previous inspection while equation (2) is used when data does exist from a previous inspection.

The frequency of inspection, based on predicted useful remaining life (L), can be established as follows:

Life Remaining (L) Inspection Interval (yrs) (yrs) 1 to 3 1 l 4 to 12 L-2 l

Any area with a useful remaining life of greater than 12 years will be inspected at a frequency dependent on inspection result of similar areas. No specific program guidelines have been established for areas with a predicted useful life greater than l'2 years.

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ATTACHMENT IEB 87-01 RESPONSE Page 5 It should be pointed out that this type of inspection program is based on .a percentage of the total possible number of exam areas. As more experience is gained in the area of erosion-corrosion within the industry and at FBHP, the sample size and the sample members may be altered.

Since no previous data existed for wall thickness measurements prior to 1987, the wall loss rates and the predicted useful remaining life values used in this report are extremely conservative. The wall loss rates presented for all exam areas were calculated in accordance with equation (1) above. It was assumed th:t all of erosion-corrosion took place over the last 5 years instead of the total 17 year operating history i' PBNP Unit 1. Also, it was assumed that at the beginning of its service life the components wall thickness was the greater of either tne standard ASTM nominal wall thickness or the average of the highest 2 to 3 wall thickness measurements taken. By allowable fabrication tolerances, as specified in the ASTM standards, it is quite possible that the pipe or fittings originally installed had a wall thickness that was as low as 12.5% below the specified nominal wall thickness. Taking these factors into account, the actual predicted useful remaining life could be as much as 5 times greater than that listed in this report.

Although a predicted life of 0 or 1 year may be assigned to a given area, it is highly likely that the actual remaining life of the component will be considerably more than that reported. However the values for wear rate and predicted useful remaining life provide a good relative comparison for determination of inspection intervals.

c. Examination Techniques For Measuring Wall Thickness Wall thickness measurement are taken using A-scan UT techniques. Each area to be examined for wall thickness is sectioned by procedure into small grid spaces and each grid space is scanned 100% with UT. The minimum wall thickness for each area is noted for each area on a data sheet. Figures A-2 and A-3 depict a typical grid system used for wall thickness measurements.

The A-scan UT technique was chosen to overcome the shortcomings of digital readout UT devices. Digital readout UT devices which do not provide a presentation of the reflected sound energy, may misrepresent small sites of thinned areas or the edge of a larger thinned area.  !

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ATTACHMENT IEB 87-01 RESPONSE' Page 6

d. Basis For Replacement / Repair Decisions ,

Pipe wall thinning, as indicated by NDE, is rejectable according to the following . criteria, unless a detailed evaluation can justify continued operation.

(1) -Reject'and repair the pipe if wall thickness is less than the

' minimum allowed by USAS B31.1 - 1967.

(2). Reject and repair the pipe if wall thickness, minus annual wear, is less than the minimum allowed by USAS B31.1 - 1967.

If signs of erosion-corrosion are present, but the remaining useful life of the piping component is greater than 1 year, the piping component may be placed back in service for I additional year. Following this period of service the piping component will be reinspected and evaluated as before.

Other areas exhibiting erosion-corrosion, but with a useful remaining life of greater than 2 years, will be reinspected as described in Response 2(b).

Those areas that have a predicted useful remaining life of less than 2 years will be seriously considered for replacement and/or repair as the need warrants.  !

Request 3 For liquid-phase systems, state specifically whether the following factors have been considered in establishing your criteria for selecting points at which to monitor piping thickness (Item 2a):

a. Piping material (e.g., chromium content)
b. Piping configuration (e.g., fittings less than 10 pipe diameters apart)
c. pH of water in the system (e.g. , pH less than 10)
d. System temperature (e.g., between 190 and 500 F)
e. Fluid bulk velocity (e.g. greater - than 10 ft/s)
f. Oxygen content in the system (e.g., oxygen content less than 50 ppb)

Response 3 Erosion-Corrosion Badness Factor A qualitative ranking of a given area's susceptibility to erosion-corrosion, relative to other areas within a given piping system, can be made through the use of a badness factor. The badness factor takes into account fluid ,

temperature, steam quality, geometry, and flow velocity. The erosion-corrosion badness factor used for the PBNP inspection program was based on the Keller Equation described in EPRI report NP-3944, " Erosion-Corrosion in Nuclear Steam Piping: Causes and Inspection Program Guidelines."

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' ATTAODfENT IEB 87-01 RESPONSE Page 7

.The erosion-corrosion badness factor, mee, can be calculated as follows:

mee = (mft)x(msx)x(mke)x(me) mft = temperature factor from Figure A-4

.msx = steam quality factor x =. Steam quality for two-phase flow use (1-x)*5 for subcooled flow use 1 L mke = geometry factor.from Figure A-5 if flow is disturbed (the upstream flow is not through straight pipe for at least 10 pipe diameters) multiply mke by; 0.5 if low disturbance 1.0 if medium disturbance i 2.5 if high disturbance me = Velocity in ft/sec The use of a factor for oxygen concentration and pH was not included. It was assumed, for all cases, that the relative contribution of these factors to the badness factor is the same for all exam points. In other words, variations in pH or oxygen concentrations are not used to further limit the selection sample size.

The badness factor relationship, described previously, is applicable only for carbon and low alloy steels. ;The badness factor is set equal to 0 for austenitic stainless steel due to its proven immunity to erosion-corrosion.

Request 4 Chronologically list and summarize the results of all inspections that have been performed, which were specifically conducted for the purpose of identifying pipe wall thinning, whether or not pipe wall thinning was discovered, and any other inspections where pipe wall thinning was discovered even though that was not the purpose of that inspection.

a. Briefly describe the inspection program and indicate whether it was specifically intended to measure wall thickness or whether wall thickness measurements were an incidental determination.
b. Describe what piping was examined and how (e.g., describe the inspection instrument (s), test method, reference thickness, locations examined, means for locating measurement point (s) in subsequent inspections.)

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ATTACHMENT IEB 87-01 RESPONSE )

Page 8

c. Report thickness measurement results and note those that were identified as unacceptable and why.
d. Describe actions already taken or planned for piping that has been ,

found to have a nonconforming wall thickness. If you have performed l a failure analysis, include the results of that analysis. Indicate l whether the actions involve repair or replacement, including any '

change of materials.

' Response 4 l The response to the above request will be in two parts. The first part vill be a summary of the pre-1987 inspection and repair program associated with erosion related piping damage. The second part will be a detailed account of the newly installed erosion-corrosion monitoring program.  ;

a. Pre-1987 erosion inspection and repair program.

At PBNP, considerations regarding the erosion of carbon steel steam piping have been addressed for nearly 15 years. Through careful and responsible l maintenance efforts, no eroded pipe or component has resulted in a l catastrophic failure. Minor through- wall leaks have occurred during the 1 17 and 15 year operating histories of PBNP Units 1 and 2 respectively. The j first recorded case was in 1973, 3 years after Unit 1 went into operation. l A through-wall leak wat observed in a 12" extraction line with a nominal l wall thickness of 0.437 inches. In only 3 years time, the wet steam had eroded through the carbon steel pipe wall at a rate of 0.147 in/yr. As a 1 result of prompt maintenance action, however, major pipe failures have been avoided.

As a result of several extraction line failures in the utility industry, PBNP undertook an extensive inspection program to assess the condition of the Unit 1 and 2 extraction lines. The program was conducted during the Fall of 1982 and the Spring of 1983, for Unit 2 and Unit i respectively.

Wall thickness measurements were taken on all areas within the extraction lines that were considered potentially susceptible to two-phase erosion-corrosion.

The results of the inspection indicated that extensive two-phase erosion-corrosion was occurring at the elbows and tees in the extraction lines, The extraction lines were fabricated from components with the following characteristics:

Nominal ASTM Pipe Component Nominal ASTM Size (in) Type Wall (in) Spec 12 Pipe 0.438 A106GRB Fittings 0.438 A234GRB 18 Pipe 0.438 A106GRB Fittings 0.438 A234GRB

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" ATTACHMENT.

.IEB 87-01 RESPONSE.

.Page 9:

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'Some elbovs inspected had local measured wall thicknesses as low as 0.060 finches. This amounted to a wall loss rate of 0.031 in/ year if a 12 year operating history is assumed.

' Prior to' returning the units to service, all areas that were thinned significantly were reinforced with welded pipe patches. In 1984.all of the extraction lines for' Unit -1 and' 2 were replaced with ASTM A312 TP304 stainless steel piping and fittings. Since stainless steel of this type is immune to'erocion corrosion, the problem of wall. thinning in the extraction

-lines was eliminated.

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.Two-phase. erosion-corrosion of the carbon steel (A53 GRB) turbine crossunder lines has been noted since the early days of. plant operation.

Local wall thinning has been significant enough to penetrate the 0.500 nominal wall carbon steel crossunder line. The first reported case of this

~ was in 1979 on Unit 1, when a through wall leak occurred on an elbow.

Annual visual inspections of the crossunder piping supplemented with UT wall thickness measuremen#.., are conducted from the inside surface to identify areas requiring sepair. Repairs are made during the annual refueling / maintenance outage as the inspection results dictate.

To reduce the erosion-corrosion rate of the turbine crossunder piping, moisture removal equipment has been installed in Unit 1 (Spring 1987) and will soon be installed in Unit 2 (Fall.1987). This equipment removes a large percentage of the entrained water from the high pressure turbine exhaust before it. enters the crossunder piping. The steam quality in the crossunder piping is therefore improved and the risk of erosion-corrosion damage to the piping is reduced substantially.

b. Current erosion-corrosion inspection and repair. program (1) Program description The current erosion-corrosion' inspection / maintenance program was initiated during the 1987 Spring Unit 1 refueling / maintenance outage.

The purpose of the inspection program is to detect and quantify significant service related degradation in.the piping systems and pre-existing conditions that could jeopardize the integrity of these systems in the future. Representative areas of systems are inspected with various NDE techniques to detect such degradation and conditions.

The underlying objective of the inspection program is to look at piping system whose failure could result in significant hazards to personnel or equipment daiaage, of those systems, areas most susceptible to service related failures are targeted for inspection.

The primary concern is to locate areas of severe erosion corrosion in carbon steel piping prior to tL' occurrence of a leak or catastrophic rupture.

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ATTACHMENT IEB 87-01 RESPONSE Page 10 Piping in the following systems were inspected for evidence of erosion-corrosion

during the 1987 Unit 1 refueling 14 outage.

1 Main Steam 1 Turbine Exhaust ~and Crossunder {

Rad Waste Steam j Extraction Steam i Feedwater Heater and MSR Drains '

Main Feed Condensate 115 inspections were conducted using A-scan UT techniques as previously l

- described in Response 2c. In addition, direct visual examinations of large diameter pipes (i.e. crossunder' pipes) were performed from the inside surface to supplement the UT exams.

Each exam area was uniquely identified with a number such as MS-24-EB-01-1102. To permit accurate location of the exam areas, isometric drawings, showing each individual exam area within a piping system, were developed.

To permit repeatability of successive wall thickness measurements on sections of a piping component, a gridding methodology was developed. By procedure, a grid system was drawn on the outside surface of the piping component. The area within each grid section was scanned 100% with UT instrumentation and the minimum observed wall thickness was recorded.

This was done for each grid section. This method will provide repeatability from year to year and will provide complete coverage of the piping components entire pressure retaining wall.

(2) Results Of Inspections 1987 Unit 1 (a) Thickness Measurement Summary Several areas were discovered to have observable wall thinning.

Most notable were the turbine crossunder lines which had extensive areas of tiger striping (Figure A-6) and erosion damage. Some areas had wall thinning of up to 50% of the original nominal wall. As noted in 4a above, turbine crossunder >

' lines have been observed to have had significant erosion-corrosion problems for many years and have necessitated annual inspections and repairs at Point Beach. Thus, the w 2; losses observed during the U1R14 inspections were expected.

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ATTACHMENT IEB 87-01 RESPONSE Page 11 Of the 23 areas inspected in the crossunder lines, nearly all of them had some indication of-thinning. Three areas had worn to the point where repairs became necessary. Figures A-6 through A-8 are examples of the type of erosion noted in the crossunder lines.

Wall thinning was also noted in some of.the main steam, main feed, and feedwater heater drain lines. Eleven areas inspected showed varying degrees of evidence of wall thinning, but none were significant enough te require immediate attention. The areas that showed evidence of wall thinning were at locations where geometries changed such as at tees and branch connections.

A summary of the inspection results can be found in Tables B-1 and B-2.

(b) Thickness Measurement Specifics i MS-40-XX-01-1126, 40" straight section near turning vane, Location: 40" crossunder line from HP turbine to MSR C ASTM nominal wall thickness: 0.500 in.

Measured nominal wall thickness: 0.550 in. l Measured minimum wall thickness: 0.330 in.

Description:

This area had extensive tiger striping in a 24 inch band from the 3 o' clock to the 9 o' clock positions. The majority of the erosion was near the turning vanes. The maximum wall loss and average wall loss observed were 34% and 16%

of nominal wall thickness respectively. This area will be reinspected in 1988.

ii MS-36-XX-01-1102, 36" elbow near turning vane, Location: Crossunder line to MSR C ASTM nominal wall thickness: 0.500 in.

Measured nominal wall thickness: 0.570 in.

Measured minimum wall thickness: 0.370 in.

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ATTACHMENT IEB'87-01 RESPONSE Page 12

Description:

This area had extensive areas of erosion around a repair weld by the turning vane. Damage was noted around the entire perimeter of the pipe ID. The most extensive erosion was noted between the 11 o' clock and I o' clock positions.

The maximum wall loss and average wall loss were 60% and 12%

of the nominal wall thickness respectively. This area was repair welded.

iii MS-40-XX-01-1110, 40" small angle elbow, Location: Crossunder line from HP turbine to MSRs A & C l ASTM nominal wall thickness: 0.500 in.

Measured nominal wall thickness: 0.550 in.

Measured minimum wall thickness: 0.300 in.

Description:

Extensive erosion was noted near cladded repaired areas.

The maximum wall loss and average wall loss were 40% and 15% of nominal wall thickness respectively. This area was repair welded.

iv MS-40-XX-01-1106, 40" small angle elbow, Location: Crossunder line from HP turbine to MSRs A & C ASTM nominal wall thickness: 0.500 in.

Measured nominal wall thickness: 0.510 in.

Measured minimum wall thickness: 0.260-in.

Description:

Extensive erosion was noted near cladded repaired areas.

The maximum wall loss and average wall loss was 48% and 16%

of nominal wall thickness. This area was repair welded.

v MS-40-XX-01-1108, 40" straight pipe section near manway, Location: Crossunder line from HP turbine to MSRs A & C l

ASTM nominal wall thickness: 0.500 in.

Measured nominal wall thickness: 0.570 in.

Measured minimum wall thickness: 0.390 in.

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ATTACHMENT j

.IEB 87-01 RESPONSE LPage 13

Description:

Erosion was noted near cladded repair areas and in the 5 o' clock to 7 o' clock positions. The maximum wall loss and average wall loss were'34% and 16% of nominal wall thickness respectively. This area was repair welded.

vi CS-16-DB-01-1029, 4" branch connection Location: B main feed pump recirc line ASTM nominal wall thickness: 0.258 in.

Measured nominal wall thickness: 0. 3': in. I Measured minimum wall thickness: 0.28v in.

Description:

Wall thinning, as indicated by UT, was noted on the branch connection pipe just downstream of the pipe to nozzle weld.

The maximum wall loss was 15% of the measured nominal wall thickness. The variations in wall thickness noted are within the original fabrication tolerances specified under ASTM A106 GRB. It is therefore possible that this condition has existed since the piping was initially installed.

vii CS-20-DB-01-1019, 20" tee Location: Main feed inlet to 5A feedwater heater ASTM nominal wall thickness: 1.28 in.

Measured nominal wall thickness: 1.40 in.

Measured minimum wall thickness': 1.00 in.

Description:

Wall thinning, as indicated by UT, was noted on both ends of the run of the tee, and the-attached piping. The maximum wall loss noted was 28% of the measured nominal wall thickness. By a conservative estimate of the wall loss rate, the predic'ed t wall thickness will reach the minimum required wall thickness within one year.

It should be noted that the predicted useful remaining life of this fitting was based on an operating history of 5 years and an original wall thickness of 1.40 in. It is quite possible that the original wall thickness in this area of concern was as low as 1.12 in. (87.5% of ASTM nominal wall thickness), and the period over which erosion-corrosion occurred was 17 years. The predicted useful remaining life, using these assumed conditions, would be 3% years. Although repair was not immediately necessary, this area will be reinspected in 1988 to more accurately assess the predicted useful remaining life.

ATTACHMENT IEB 87-01 RESPONSE Page 14 viii CS-20-DB-01-1115, 20d tee Location: Main feed to feed regulating valves ASTM nominal wall thickness: 1.28 in.

Measured nominal wall thickness: 1.25 in.

Measured miniinum wall thickness: 1.03 in.

Description:

Wall thinning, as indicated by UT, was noted on both ends of the run of the tee, and the attached piping. The maximum wall loss was 20% of the nominal wall thickness. By a conservative estimate of the wall loss rate, the predicted wall thickness will reach the minimum required wall thickness in approximately one year. This area will be reinspected in 1988.

ix FD-10-GB-02-1116, 10" tee Location: MSR C drain to 5B feedwater heater ASTM nominal wall thickness: 0.593 in.

Measured nominal wall thickness: 0.460 in. l Heasured minimum wall thickness: 0.400 in.

Description:

Wall thinning, as indicated by UT, was noted on the run of the tee. The maximum wall loss noted was 32% of the nominal wall thickness. The predicted useful remaining life of this fitting based.on a conservative wall loss rate of 0.038 in/yr, is 7 years. Based on the degree of wall loss and the uncertainty of the wall loss rate, this fitting will be reinspected in 1989.

x FD-12-GB-03-1005, 22" elbow Location: Common heater drain tank pump discharge line ASTM nominal wall thickness: 0.375 in.

Meesured nominal wall thickness: 0.303 in.

Measured minimum wall thickness: 0.280 in. j

Description:

Wall thinning was noted on the pipe section immediately i downstream of the inside radius of the elbow. The maximum wall loss was 25% of the nominal wall thickness. The ,

predicted useful remaining life, based on a conservative l wall loss rate of 0.019 in/yr, is 3 years. Based on the degree of wall loss and the uncertainty of the wall loss i rate, this fitting will be reinspected in 1988.

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ATTACHMENT i IEB 87-01 RESPONSEL Page 15' xi CS-06-EB-09-1002, 6" elbow Location: Main feed line downstream of "A" feed regulating bypass valve ASTM nominal wall thickness: 0.432 in.  ;

Measured nominal wall thickness: 0.405 in. l Measured minimum wall thickness: 0.340 in.

Description:

Wall thinning was noted on the outside radius of the elbow.

The maximum wall loss was 21% of the nominal wall thickness.

The predicted useful remaining life, based on a conservative wall loss rate of 0.018 in/yr, is 3 years. Based on the degree of wall loss and the uncertainty of the wall loss rate, this fitting will be reinspected in.1988.

xii FD-10-HB-03-1212, 10" tee Location: 5B feedwater heater drain line ASTM nominal wall thickness: 0.365 in.

Measured nominal vall thickness: 0.395 in.

Measured minimum uall thickness: 0.290 in.

Description:

Wall thinning was noted on the branch of the tee. The maximum wall loss was' 26% of the measured nominal wall thickness. The predicted useful remaining life, based on a conservative wall loss rate of 0.021 in/yr, is 11 years. Based on the degree of wall loss and the uncertainty of the wall loss rate, this fitting will be reinspected in 1989.

xiii FD-08-HB-05-1004, 8" tee Location: 3B feedwater heater drain line ASTM nominal wall thickness: 0.322 in.

Measured nominal wall thickness: 0.330 in.

Measured minimum wall ~ thickness: 0.260 in.

ATTACHMENT IEB 87-01 RESPONSE Page 16

Description:

Wall thinning was noted on the branch of the tee. The maximum wall loss was 21% of the measured nominal wall thickness. The predicted useful remaining life,_ based on a conservative wall loss rate of 0.014 in/yr, is 17 years. Based on the degree of wall loss and the uncertainty of the wall loss rate, this fitting will be reinspected in 1990.

xiv CS-20-58-04-1007, 20" elbow Location: Main feed pumps common suction line ASTM nominal wall thickness: 0.375 in.

Measured nominal wall thickness: 0.375 in.

Measured minimum wall thickness: 0.310 in. '

Description:

Nall thinning was noted on the outside radius of the elbow.

The maximum wall loss was 17% of the nominal wall thickness.

The predicted useful remaining life, based on a conservative wall loss rate of 0.013 in/yr, is 3 years. Based on the degree of wall loss and the uncertainty of the wall loss rate, this fitting will be reinspected in 1988.

xv MS-30-EB-01-1306, 30" tee Location: Main steam line upstream of non return valve ASTM nominal wall thickness: 0.908 in.

Measured nominal wall thickness: 1.570 in.

Measured minimum wall thickness: 0.960 in.

Description:

Wall thinning, as indicated by UT, was noted on the branch portion of the tee. .The maximum wall loss was 38% of the measured nominal wall thickness. By a conservative estimate of the wall loss rate, the predicted wall thickness will reach the minimum required wall thickness in one year. It should be noted that the wall thickness variations noted are within the original fabrication tolerances of ASTM A155. ,

It is therefore possible that this condition has existed since the piping was originally installed and no wall thinning has actually occurred. This area will be reinspected in 1988 to confirm this.

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ATTACHMENT  !

IEB 87-01 RESPONSE Page 17 xvi CS-20-DB-01-1010, 20" to 16" reducing tee  !

Location: Inlet to SB feedwater heater ASTM nominal wall thickness: 1.28 in.

Measured nominal wall thickness: 2.10 in. j Heasured minimum wall thickness: 1.18 in. '

Description:

Wall thinning, as indicated by UT, was noted on the run of the tee. The maximum wall loss was 44% of the measured nominal wall thickness. By a conservative estimate of the wall loss rate, the predicted wall thickness will reach the minimum required wall thickness in one year. It should be noted that the variations in wall thickness noted are within the original fabrication tolerances specified under ASTM .

A106 GRB. It is therefore possible that this condition has existed since the piping was originally installed and no wall thinning has actually occurred. This area will be reinspected in 1088 to confirm this.

Request 5 Describe any plans either for revising the present or for developing new or additional programs for monitoring pipe wall thickness.

Response 5 The current inspection program was implemented for the first time during the 1987 Unit 1 refueling outage. It will also be used for the upcoming 1987 Unit 2 refueling outage. As the current program is based on EPRI report 3944 and existing WE and industry experience, it is likely changes will be made to the program as new information becomes available.

Once the most susceptible areas for erosion-corrosion have been clearly identified, and reasonable erosion-corrosion wall loss rates established, the  ;

s.,ple size and its constituents may be revised. Our inspection policy has been conservative to ensure that PBNP Units 1 and 2 are operated in a manner that will ensure the safety of the public, operating personnel, and plant ,

equipment. l l

4 l

l l

I l

_-_________ - _ a

ATTACIIMENT-IEB 87-01 RESPONSE

SECTION A Page 1 Ih I/

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P C/Ai 7* 7 WOut.b Bf DEC)GNATEb CS-/6 -E8-09 -/ 007 FIGURE A-1

ATTACHMENT j IEB 87-01 RESP 0llSE j SECTION A Page 2 .

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FIGURE A-3 Grid shown on 10" tee i

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1 ATTACHMENT

2EB 87-01 RESPONSE SECTZON A.

  • Page 3

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50 100 150 200 250 TEMPERATURE 'C NOTE: f(t) IS PROPORTIONAL TO CORROSION RATE F1GURE A-4 Influence of Temperature on Erosion / Corrosion in Two-Phase Flow l

i

ATfACHMENT l :IEB 87-01 RESPONSE l

E SECTION A Page 4

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FIGURE A-5 Influence of steam-path configuration on erocion-corrosion

1

- ATTACHMENT I IEB 87-01 RESPONSE SECTION A Page 5 , m e - - 4 gg  ; ;g 7 47 i;?fhjjl:, a , -l&.:. ,

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FIGURE A-6 Tiger striping type erosion noted in I crossunder lines

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FIGURE A-7 Erosion damage near cladded area

4 ATTACHMENT IEB 87-01 RESPONSE l SECTION A Page 6

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l

  • " ATTACHMENT IED 87-01 RESPONSE SECIION B TABLE B-1 UT WALL THICKNESS INSPECTION

SUMMARY

Key Column Heading Description.

Exam Point Unique identifier for each exam area (Reference Table B-4)

Config Type of component SP - Straight Pipe LB - Lateral Branch LJ - Lateral Junction TB - Tee Branch E- Elbow SRE - Short Radius Elbow LRE - Long Radius Elbow W- Weld 0- Other l

Exam Method NDE Hethod UTT UT wall thickness measurement UTW UT weld inspection l MT Magnetic particle inspection DT Dye penetrant inspection Procedure NDE procedure Data Sheet Data sheet ID number Disposition Disposition of finding R - Repaired NR - Not Repaired Engineering Evaluation Required An "X" indicates that an engineering evaluation was required.

I Reference Isometric Drawing Isometric drawing on which the exam l point can be found Remarks Pertinent comments Life Expect Predicted useful remaining life L

l l

'h^8 $

TABLE B-1 3, Page No. 1 '

98 /26 /87 - j.

2 J UfWALLfHICINESSHIP0tf [

LIFE IIANPOINT' CONilG.IIAH PROCID0tt DATASHI!f DISPOSifl0llINGINill!NG BtflitNCE HENAltt? 1 18780D N m" IVALUAf!0N ISOHIfRIC  !!PICf.

RIQOlf!D LRAWING o<.

104019 10 CS-14DB01-1001f Off NDI104 ._

i 5

.C8-14DB011003I -Off NDI-104. 14018 Off HI104 101-081 '+ 3 CS-12-DB-0110050 7

CS-16 DB-01100$ I Off NDI-104 104 110 Off .HDE-104 104 109 REINSPICf88 1  !

CS20DB-011010.LB-9 CS-1248-01101J 0 Off El104 104-052 CS-20DB-011019fB Off . El104 104-02D HN BIINSPICT88 0 )

i 6

' CS 1648 011029 LB Uff E l-10 U 10( 019 14 l CS16-DB-01-1038I Off nDI13(L: 194 i66 104 067 17 05-164B-01 1045 I Off - NDE 104 29 CS16DB01-i103I Off NDI-104 104 111 REINSPECf88 1

. CS-204B-011115 fB Uff NDE 104 '104 083 2

. CS444B 021232 LB Off HDI-104 104 068 ' '

DEL!f!D 0

^HS24-IB-01-1012SP Off NDE-104

~HS-24IB011101W Off El-104 104-113 T LILitID 0 Y;

NT NDI-350 350034 OfW G1-105 105039 It!NSPECT88 6 IS24IB011102LB . 0ff NDI104 104-112 5

HS30IS-011220LB Off HI104 104-005 REINSPICT88 1 HS30IB-011306fB Off NDI104 104-127 Hi104 104-108 6 s 8S-1818-0210010 Off 2

- BS-24IB-02-1001LB Off HDI104 104 126 6

ES-24-IB-02-1004I Off . El 104 104-094 2

HS06IB021006I Uff NDE104 104-097 Off NDE-100. 104-128 2

FD-06-tB-06-1419 fB Uff H1104- 104-013 Uff - HI104 104-129 3

TD-06-IB-06-1430t Off HI-104 104-078 5

161B-091002I Off HDE104 104064 REINSPICf68 3 CS-06-IB-09 1002 I Off HI104 104 471 6

CS 16 tB-091005 I Off El104 104010 8

.CS-16-tB-091006LJ Uff HDI104 104-104 14

- CS16IB091032I Off NDI104 104125 8 '.

CS16IB091035I Off NDI 104 104 124 i

3 CS16-tB091943 SRI Off IIDI104 104-00 0 CS16IB-09-1059I Off DB-104 104-002 4 l 6 l C5161B091061LJ Off NDI104 104007 6 l 05161B-09-1102I Off NDI104 104-072 g ,

pl104 9 CS06-IB-091102I' Off 104105 2 l CS16IB0911051 Off NDE104 104-095 2 1 CS16!B091108LJ Off HE-104 104106  !

CS-16-tB49-1111 I Off .HI104 104-107 8 I

5 CS16IB-09-1130I Off IDI104 104-123 i

3 CS 16 IB-09-1133 I Uff NDI104 104-122 4

CS-16 IB 091152 SHI Off DE104 104-056 05-13-18 4 9-1161 I Off 8810( 104011 10 4

CS16-IB-091182I Off HI-104 104 003 5

CS 16 tB 09 !!86 I Off El-104 104-001

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! 08/36/87 -  !

OfIIALLTHICINESSIIP0Hf IIAlj@f CONF!G. IIAN - P100tD01t DafASBitt DISPOSlfl0N ENGINIIRING HlfilINCE RINARIS Lift EVALDAf!0N ISONIf81C IIPICf.

, Q~C7 NtfBOD '

J 18Q0188D ' DRAWING 4

$316IB-09-li88LJ Off ' NDE104 104006 50

FD-10-GB-02-1021 Bf ~ Off NDE 104~ 104 062 46

- TD-10 GB-021108 7J Off' NDR-104' 104061 REINSPECf 1989 7 FD-10-GB-02-1116.LB Uff NDE-104 . 104 014-HDI-104 104-063' 30 170-100802-1120BT Off Off NDI-104 104-066 ,

-Off .NDE-104 104-033 HEIN8PICf1988 3 gri9-12GB-031005 SRI

.10-10G8-03-1007I Off 'HDE104 104-024 ~ 10 10  !

FD12GB-03-1017I 077 NDE-104 104-028 Off. NDI104 104-130 20  :

18 08-04 1000 '

Off NDE104 104-044 11 CS-18GB-041001788 Off- NDE-104 104-008 9  ;

.CS-12 CB 04 1905 I CS-20-GB-0(1007SBt Off  !!DE104 104-087 tilllSPECf 1988 3 CS-18-GB04-1010 SRI Off 1101104 104-039 12

05-12-08 04 1013 I Off ND8104 104-009 13

'CS-18GB-041014SHI: Off NDE10( 10(-031 B CS-12 GB-041123 I- Off NDI-104 104-077 15 CS-12-GB-04-1211LB Off NDE-104 104-065 12 TD08-GB05-il26LB- Off NDE104 104-041 21 Off 108-104 104-040 (8 4 -fa 08 GB-05-ll28 SRIOff .NDE-104 104-032

39-98 08-05-1214 Sit 15 W'FD-08-GB-05-1231LB Uff IIDI 104 3104-047 16 l tFD08GB-051233 SRI Off NDE-104 104046 33 CS-18-GB-07-1011 SHI Off NDE-104 104099 4 68-18 GB-071016 LB Off HDE104 104-100 9 CS-18 GB-07 1017 Il Off NDE-104 104-101 6 CS 10-GB-071022 SRI Off IIDE104 104038 9 CS-18GB-071036 Sit Off NDI-104 104037 7 CS 18-GB 07-1041 LB Off NDE-104 104 043 3 CS 10-GB 07-104211 Off IIDI-104 104-085 20 NS12GD-01-1132I Off 104-091 Dillf!D 0 NS-12-GD-01!!35i Off NDE104 10(-092 DILITID 0 NS-12GD01-1251I Off NDI104 104-093 DELifkD 0

'FD08BB-01lll9fB Off 1t4-057 DELiflD 0 F916HB021018 Sit Off NDE-104 104-080 19 TD-10 CB 03-1112 LB Off NDE-104 10(-074 24 FD-10HB-031212LB Off ND8104 104-073 REINSPECT 1989 11 FD08HB-0(-1003 SRI Off NDI104 104098 21 FD-12HB041005I Uff NDE:104 104070 25 FD-12HB041013I Uff NDI104 104-096 23

.FD-08-HB05-1004LB Off NDI104 101-075 tilNCPECf1990 17 TD-06 B 05 1068 0 Off NDI-104 104-088 59 TD-12CB-18-1003I Off NDE104 104-042 51 10(027 12 TD 14 HB-18 1005 I Off NDI-104 Off IIDI10( 104045 13 FD-12 HB-18 1006 I FD-14HB-181008SP Off liDE-104 104030 20 FD-14BB-18-1009LB Off 104076 DELIftD 0 FD 12 HB-18 1011 I Off NDE104 104-050 32

c + .

, PageNo; ~3

  • 08/26/87 OfWALLTHICINISSREPORf IIANPOINT CONFIG. IIAH PROCIDUll DifASLitt DISPOSit!0N ENGill!BING Billa!NCE BIBAl[S LIFE MtfBOD If!LDAfl0N IS0Hittl0 IIPICf.

REQOlltD DRAWING L

7914-BB-181014 I Utf NDI-104 104 026 19 FD-12HB181014I Off HDE-104 104-051 26

'fD-12HB181017I Off NDE-104 104-035 14 FD-1248-181022 LB ~ Uff NDE-104 104 069 19 FD-14HB-18-1023I Uff NDI-104 104-025 20 FD-12-BB-181024 I- Off NDE-104 104052 23 F3-12-BB-18-102i! Off IIDI104 104-034 16 HS 10-HD-04-1123 ^ Off 104-058 DELifID '0 HS18HD-04-11270 Off 104-060 DELIf!D 0 H518-H0-0412280 Off 104059' DIlif!D 0

,,RS 03-SA 60-Il66 I 36 Off NDE-104 104 054 10 IS 03-SA-60-1170 0 Uff NDI104 104055 NOT!!AMINID 0 ,

1S-03SA-60-1178I Off HDE-104 104-053 DDETOHlif HH6-II-01-1102I Off NDE104 104021 R REPAlllD 4 3DI-104 104115 20 i H5-291101-1104LB . Off '

10H17 11

.85-29-II-01!!05LB 177 1101104 HS-40-II-01!!06LII Off HDE104 104048 8 REPA! RID 1 HS-29-II-01-1106LB Off NDI 104 , 104 118 DILif2D 0 Off 10110( 104029 8 53-3611-01-1108I HS40II-01-1108LB Uff NDE-104 104049 R RIPAIRID 5 HS49-II011110LRE Uff NDI104 104036 R HIPAltID 2 HS29!I01-1110t Off NDE-104 104-114 5 4  !

H5-40I!01-1117LB Uff NDE-104 104-015 H540-I10111190 Uff El-104 104016 2 .,

4 1 H529-I!011125LJ Off NDI-104 10(-116 MS29IIOlll26LB Off HDI-104 104017 NH RIlllSPICT 88 4 HS-40-!!-0112010 Off XDI-104 104102 6 HS29!!011202W Uff NDE-104 104 121 3 HS-36-II01-1205LB Uff HDI-104 104-022 4 ,

MS36-II011206LB Off NDE104 104023 4 HS-40-II011207LB Uff DNI-10( 104-090 4 HS-40-II01-1209I Uff IIDI-104 10H84A DOWISTRIABSIDE 4 j HS29II-011209I Off NDI104 104103 8 HH0II-01-1209I DPSfilABSIDI <

Off NDI104 104084B 5 MS29-II-011217LB Off NDI104 104-119 24 HS 29-II-011218 LB Off NDI-104 104 120 6 HS-N II-01 1222 LB Off NDF104 104 089 5 q

i i

l

.i

' ATTACHMENT IFB 87-01 RESPONSE SECTION B 1

l- Table B-2 UT WALL THICKNESS CALCULATION RESULTS i- Key l

l Column Description Exam Point Unique identifier for each exam area l (Reference Table B-4)

ASTM Nominal Wall Nominal wall thickness as specified in ASTM standards Heasured Nominal Wall Greater of the ASTM nominal wall i thickness and the average wall l

thickness derived from the highest

two or three wall thickness measurements taken.

Calculated Minimum Wall The minimum required wall thickness as calcu3ated by code formulas.

Heasured Minimum Wall Minimum wall thickness noted within the exam area.

Average Wall Thick Averagc wall thickness within the exam j area. -

Local Wear Rate The wear rate observed at the point of minimum wall thickness.

General Wear Rate The average wear rate. observed over the entire exam area.

Extent The percentage of the exam area.that is exhibiting erosion. This factor is only applicable to the turbine crossunder lines.

Life Expect Predicted useful remaining life.

NOTE: THE LOCAL WEAR RATES CALCULATED FOR ALL EXAH AREAS INSPECTED DURING THE 198', U1R14 OUTAGE WERE DETERMINED IN ACCORDANCE WITH EQUATION (1) .

IN RESPONSE 2b. .!

1 l,

l

4

?ageN.' 1 TABLE B-2 4 08/!6/87 i

OfWALLTHICINISSI!P0tt CALCULATIONS E!AHPOINT AStuHEASURIDCALCOLAf!DHIASOHIDli!BAGt LOCAL GINERA1,!!7ENT Lill NOMINAL N08INAL HINIB05 HINIHW WALL WIAR Will (1)IIFICf.

WALL WALL WALL WALL fBICE. Haft RATI (TH.)

(!h.) (IN.) (IN.) (IN.) (IN.)(IN/TR) (IN/fR) l CS-14-DB-01 1001 0.9370 0.950 0.684 0.870 0.920 0.0260 0.0140 0 10 0514-03-01-1003 0.9380 1.030 .0.684 0.870 0.920 0.0600 0.0500 0 5 CS-12-DB-01-1005 1.0310 1.150 0.781 0.940 0.980 0.0420 0.0340 0 3 CS-13-DB01-1005 1.0310 1.050 0.781 0.940 1.010 0.0220 0.0080 0 7 CS-29-DB-01-1010 1.2800 2.100 0.976 1.180 1.690 0.1840 0.0820 0 1 CS12-DB-01-1010 1.0310 1.120 0.781 0.999 1.060 0.0240 0.0120 0 9 CS-80-DB011019 1.2800 1.400 0.976 1.000 1.250 0.1300 0.0840 0 0 CS16-DB-01-1029 0.2580 0.330 0.219 0.280 0.320 0.0140 0.0060 0 6 CS16-DB-011038 1.0310 1.100 0.781 1.020 1.070 0.0260 0.0120 0 14 CS16-DB-01-1045 1.0310 1.300 0.781 1.190 1.230 0.0240 0.0140 0 17 CS16-DB-011103 1.0310 1.270 0.781 1.200 1.230 0.0140 0.0080 0 29 CS-20-DB-011115 1.2800 1.530 0.976 1.100 1.440 0.1420 0 3400 0 1 CS-04DB-021232 0.3370 0.270 0.220 0.260 0.265 0.0150 0.0140 0 2 HS-24-IB-011012 0.0000 0.000 0.000 0.000 0.000 0.0000 0,0000 0 6 HS-24-IB01-1101 0.8680 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 HS44-IB 01-1102 0.8680 0.843 0.783 0.827 0.833 0.0080 0.0070 0 5 5530-8B01-1220 0.9080 0.950 0.908 0.930 0.950 0.0420 0.0160 0 5 HS-30-IB01-1306 0.9080 1.120 0.907 0.960 1.070 0.1220 0.1000 0 1 MS-18IB02-1001 0.7500 0.740 0.632 0.700 0.710 0.0100 0.0260 0 6 MS24-IB021001 0.8680 1.800 0.843 1.140 1.290 0.1340 0.1020 0 2 HS-24-IB-02-1004 0.8680- 1.120 0.8 H 1.000 1.0;0 0.0240 0.0140 0 6 HS-06IB-02-1006 0.2800 0.280 0.233 0.250 0.260 0.008' O.0060 0 2 FD06IB06-1419 0.2800 0.320 0.233 0.260 0.273 0.0120 0.0050 0 2 FD-06-IB-06-1430 0.2800 0.290 0.233 0.270 0.280 0.0120 0.0060 0 3 CS-16-IB09-1002 0.8430 0.880 0.675 0.800 0.840 0.0320 0.0100 0 5 CS-06IB-09-1002 0.4320 0.405 0.279 0.340 0.375 0.0190 0.0110 0 3 CS-160-09-1005 0.8(30 0.990 0.675 0.850 0.910 0.0280 0.0160 0 6 CS 16- s 09 1008 0.8430 0.980 0.675 0.880 0.950 0.0960 0.064 0 8 CS-16IB09-1032 0.8430 0.870 0.675 0.820 0.830 0.0100 0.0080 0 14 CS-16IB-091035 0.8430 0.860 0.675 0.800 0.830 0.0140 0.0060 0 8 CS-16IB09-1043 0.8430 0.870 0.675 0.760 0.810 0.0360 0.0120 0 3 CS-16IB-09-1059 0.8430 0.990 0.675 0.820 0.810 0.0340 0.0240 0 4 CS16IB-091061 0.8420 0.880 0.675 0.800 0.830 0.0180 0.0100 0 6 CS-16IB-09-1102 0.8430 0.840 0.67) 0.770 0.800 0.0220 0.0140 0 6 CS-06-IB-09-1102 0.4320 0.450 0.279 0.390 0.410 0.0120 0.0080 0 9 CS-16IB-09-1105 0.6430 0.870 0.675 0.800 0.845 0.0500 0.0160 0 2 CS-16 n-09-1108 0.8430 0.980 0.675 0.770 0.840 0.0500 0.0280 0 2 CS-16IB-09-1111 0.8430 0.820 0.675 0.780 0.800 0.0126 0.0086 0 8 CS16EB-09-1130 0.8430 0.800 0.675 0.160 0.780 0.0166 0.0126 0 5 CS-16 IB-09-1133 0.8430 0.780 0.675 0.740 0.750 0.0206 0.0186 0 3 CS-16IB-09!!$2 0.8430 0.847 0.615 0.810 0.830 0.0460 0.0200 0 4 CS-16-IB-09 1161 0.8430 1.030 0.615 0.940 0.980 0.0260 0.0100 0 10 0516-1B-091182 0.8430 1.020 0.675 0.910 0.940 0.0220 0.0080 0 4 CS-16-IB-09-1186 0.8430 1.040 0.675 0.860 0.950 0.0360 0.0180 0 5 CS16IB09-1188 0.8430 0.870 0.675 0.770 0.830 0.0200 0.0080 0 (

'f Ufage No.

  • 2 w 08/26/87 '

UtWALLTHICllt$$IIPORT CALCUL&fl0lS  ;

IIAHPOINfl AStBUIA50RIDCALCOLATIDBl&S0i!DATIBAGI LOCAL GIptlAL!!ftNT LIFE  !

50HINAL.50Hil&L ~ HINIB05 B181505 - WALL WIAR Wi&R (%) IIPICf.

WALL WALL WALL ~' WALL fBICK. RAf5 Batt _ (7R. ) .

(IX.) (IN.) (II.) (IN.) (II.)(IR/IR) (Ill/h) ,

FD-10-GB-02-1021 1.4400 1.990' l.440 1.940 1.970 0.0100. 0.0040 0 50 FD-10GB-021108 0.5930 . 0.590' 0.131 0.550 0.570 L0090. 0.0050 0 46

.fD-10-GB-02-1116 0.5630' ~ 0.460 - 0.122 0.400 0.430 0.0380 -0.0320 0 7 FD10-GB-02-1120 1.4400 1.930 1.440 1.860 1.910 0.0140 0.0040 0 30 FD-12-GB-03-1005 0.3750 0.303 0.216 0.280 0.225.0.0190 0.0160 0 3 FD-10GB031007 0,3650 0.390 0.182' O.330 0.360 0.0140 0.0060 0 to FD-12-GB-03-1017 0.3750 0.380 0.216 0.340 0.365 0.0120 0.0070 0- 10 651008041000 0.3750 0.390 0.237 .360 0.370 0.0060- 0.0040 0 20 CS-18GB04<1001 0.3750 - 0.380 0.237 0.370 0.520 0.0200 0.0100 0 11 CS 12-GB-04 1005 0.3750 0.430- 0.168 0.330 0.350 0.0180 0.0080 0 9 CS 20-GB-041007 0.375C 0.375 0.263 0.310 0.350 0.0130 0.0070 0 3 CS-18-GB-04-1010 0.3750 0.360 0.237 0.340 0.355 0.0110; 0.0050 0 12

.CS 12 GB 04 1013. 0.3750 0.420 0.168 0.350 0.330'O.0140 0.0060 0 13 CS-18GB-04-10141 0.3750 0.400 0.237 0.340 0.370 0.0120 0.0060 0 8 08 leGB-04-1123 0.3750 0.380 0.168 0.350 0.370 0.0120 0.0200 0 15 CS 12-Gb 04 1211' O.3750 0.390 0.168 0.360 0.375 0.0410 0.0160 0 12 FD-08-GB-05-1126 0.3220 0.290 0.105- 0.280 0.287 0.0080 0.0070 0 21 FD-08-GB-051128 0.3220 0.310 'O.105 0.300 0.305 0.0040 0.0030 'O 48 TD-08-GB-05 1214 'O.3220 0.300 0.105 0.290 0.295 0.0130 0.0050 0 15 FD-98GB-05-1231 0.3220- 0.315 0.105 0.270 0.300 0.0100 0.0040 0 16 FD-08GB-051233 0.3220 0.343 0.105- 0.320 0.337 0.0070 0.0030 0 33 CS-18GB-0710l! 0.3750 0,350 0.246 0.320 0.340' O.0180 0.0070 0 4 05180B-07-1016 0.3750- 0.600 0.246 0.500 0.560 0.0360 0.0200 0 9

'CS 18-CB-07 1017 0.3750 0.360 0.246 0.320 0.350 0.0110 0.0050 0 6 CS-18-GB 07 1022 0.3750 0.420 0.246 0.340 0.360 0.0120 0.0050 0 9 C5 10-08 07 1036 0.3750 0.403 0.246 0.330 0.360 0.0140 0.0070 0 7 C5100B-071041 0.3750 L90 0.246 0.420 0.557 0.1320 0.0190 0 3 l CS 10-GB-01-1042 0.3750 0.U 0 0.246 0.350 0.365 0.0050 0.0020 0 20 l HS12CD-011132 6.3750 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 BS 12-GD-01 l!35 0.3750' O000 0.000 0.000 0.000 0.0000 0.0000 0 0

. HS 12-GD-01-1251 0.3750 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 FD-08HB01!!!9 0.3220 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 FD-16-HB-02 1018 0.3750 0.395 0.079 0.350 0.285 0.01:0 0.0070 0 19

'TD-!D-HB-03-1112 0.3650 0.410 0.053 0.350 0.370 0.0120 0.0080 0 24 TD10BB-031212 0.3650 0.395  ?.053 0.290 0.340 0.0210 0.0110 0 11

'FD-08HB041003 0.3220 0.280 'O.043 0.270 0.275 0.0100 0.0040 0 21

.TD-12-CB-041005 0.3750 0.370' O.063 0.350 0.360 0.G a0 0.0050 0 25 TD-12 HB-041013. 0.3750 0.350 0.063 0.320 0.335 0.0110 0.0080 0 23 TD-08HB-051004 0.3220 0.300 0.014 0.260 0.288 0.0140 0.0070 0 17 FD-06 BB 051068 0.2700 0.270 0.011 0.250 0.260 0.0040 0.0020- 0 59 TD12-HB181003 0.3750 0.370 0.054 0.360 0.367 0.0060 0.0040 0 51 TD-14HB-181005 0.3750 0.440 0.060 0.330 0.390 0.0220 0.0100 0 12 D 12 HB-181006 0.3750 0.380 0.454 0.340 0.370 0.0220 0.0110 0 13 ID-14-HB-18 1008 0.3750 0.393 0.060 0.330 0.370 0.0130 0.0050 0 20 FD-14HB18-1009 0.3750 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 i

_ _ _ _ _ _ - _ _ _ ___.______-_.______________.___--__m.m___-m_________-______m_ - _ - . _ _ _ - _ _ _ ___ _ _ - _ _ ___.u

I '

l

!!ageno/ 3 A 08/26/87 Of WALL THICHESS IIP 0ff CALCOLAfl0lS

!!ARP0lif ASTE HtASURID CALCOLAf!D HIAS0llD FiBAGE LOCAL GtHRAL IITHf LIFI -

NOMINAL 10BIIAL' H111505 H18190H WALL WEAR WEAR (t)IIPECf.

WALL WALL WALL WALL 7H101. RATI laf! (fl. )

(IN.)- (IN.) (ll.) (IN.) (ll.)(IN/7R) (II/ft)

FD-12HB1810l! 0.3750 0.380 0.054 0.350 0.372 0.0090 0.0050 0 32 FD-H-HB-18 1014 0.3750 0.448 0.060 0.370 0.410 0.0160 0.0080 0 19

.ID-12-HB-18-1014 0.3750 0.390 0.054 0.350 0.380 0.0110 0.0050- 0 26 FD-12HB-181017 0.3750 0,427 0.054 0.330 0.375 0.0190 0.0100 0 .(

FD 12 EB-18-1022 0.3750. 0.403 0.054 0.350 0.375 0.0170 0.0070 0 19 FD-14-HB181023 0.3750 0.430 0.060 0.370 0.400 0.0120 0.0060 0 20 FD 12-HB 18-1024 0.3750 0.395 0.054 0.340 0.380 0.0120 .0.0040 0 23 FD12-IB-18-1029 0.3750 0.390 0.054 0.350 0.355 0.0180 0.0070 0 16 HS 18-HD-04 il23 0.3750 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 RS 18 BD-H 1127 0.3750 0.000 0.000 .0.000 0.000 0.0000 0.0000 0 0 8S 18 8D-04-1228 ' O.3750 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 ,

RS-03 SA-60-Il66 .0.2160 0.200 0.110 0.190 0.200 0.0030 0.0020 0 36 RS-93SA-60-Ilf0 0.7160 0.950 0.310 0.740 0.860 0.H2O 0.0180 0 10 3S03-5460-1176 0.2160 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 BS-36-II01-lM3 0.5000 0.570 0.179 0.370 0.000 0.0400 0.0000 40 4 BS29II-011104 0.5000 0.480 0. !H 0.430 0.460 0,0140 0.0080 10 20 BS29!!01!!05 0.5000 0.510 0.144 0.400 0.460 0.0220 0.0100 10 11

-HS-40!!-011106 0.5000 0.510 0.199 0.260 0.000 0.0500 0.0000 30 1 852911011106 0.5000 0.000 0.000 0.000 0.000 0.0000 0.0000 0 0 BS-36-II-01 1108 -0.5000 0.555 0.179 0.420 0.000 0.0270 0.0000- 30 8 HS40II-01-1108 0.5000 0.570 0.199 .0.390 0.000 0.0360 0.0000 20 5 i HS-40II01ll10 0.5000 0.550 0.199 .0.300 0.000 0.0500 0.0000 30 2  ;

'HS-29-II-01il10 0.5000 0.560 0.144 0.370 0.420 0.0380 0.0280 20 5  !

HS-40-II-01lll? O5000 0.50 0.199 0.370 0.465 0.0350 0.0160 20 4 8340-!!01!!!9 3.5000 '0.550 0.199 0.330 0.000 0.0H0 0.0000 30 2  :

5529-I!011125 0.5000 0.540 0.144 0.330 0.420 0.0440 0.0260 50 (

NS29II-01-ll26 0.5000 0.550 0.1H 0.330 0.000 0.0H 0 0.0000 30 4

-HS40II011201 0.5200 0.530 0.199 0.380 0.420 0.0300 0.0220 30 6 RS 29 !!-011202 0.5000 0.500 0. lu 0.300 0.400 0.0400 0.020D 50 3 HI 36 II-01-1205 0.5000 0.560 0.179 0.350 0.000 0.0420 0.0000 40 4 i BS-36-II-011206 0.5000 0.560 0.179 0.350 0.000 0.0420 0.0000 40 4 i i

-HS40-II-011207 0.5000 0.568 0.199 0.380 0.000 0.0360 0.0000 20 4

.BS40-II011209 0.5000 0.550 0.199 0.370 0.000 0.0360 0.0000 45 4 RS29-II-01-1209 0.5000 0.550 0 lH 0J00 0.000 0.0300 0.0000 40 8 HS 40-II-011209 0.5000 0.550 0.199 0.390 0.480 0.0320 0.0140 0 5 i RS-29II-011217 0.5000 0.470 0. lH 0.40 0.450 0.0120 - 0.0100 20 24 55-29-11-011218 0.5000 0.490 0.1H 0.340 0.440 0.0320 0.0120 50 6 HS29-II-01-1222 0.5000 0.550 0.144 0.360 0.000 0.0400 0.0000 40 5 l

'1 l

u 1

L_-_____-_. - _ . _ . .

ATTACHMENT IEB 87-01 RESPONSE SECTION B TABLE B-3 EXAM POINT CHARACTERISTIC

SUMMARY

Column Description Exam doint Unique identifier for each exam area (Reference Table B-4).

. Diameter Nominal pipe diameter Config Type of component

-SP - Straight Pipe LB - Lateral Branch LJ - Lateral Junction TB - Tee Branch E - Elbow SRE - Short Radius Elbow LRE - Long Radius Elbow W - Weld 0 - Other Material ASTM material spec ASTM Nominal Wall Nominal wall thickness specified in ASTM standards.

E-C Badness Factor Erosion-Corrosion badness factor Stress Badness Factor Stress badness factor Overall Badness Factor Overall badness factar

TABLE B-3

. pg yo,.y - g T 08/26/87.

IIAH FM H N ARACitt1SflCS REAHP0!lt 1 ,J COIFIG. H&ftRIAL AStu t-C-StltSSOfttALL tII.) 50H11ALBADNISSBADlitSSBADbtSS WALL FACTOR FACTOR FACTOR (II.)

CS14-DB-01-1001 14f A 106 B 0.9370 1.960 0.579 7.618 CS14DB-01-1003 14i A-106B 0.9380 1.920 0.579 13.499 CS 12 DB 01-1005 12 0 A-106B 1.0310 1.531 .0.556 6.262 CS16DB011005 16 i A106B 1.0310 3.001 0.598 10.798 CS20-DB-011010 20 LB A-106B 1.2800 6.403 0.476 20.636 05124B 01-1010._ 00 1.0310 0.000 0.000 0.000 CS20-DB-011019 20 fB A106B 1.2800 3.842 0.594 13.309-CS 16 DB-01 1029 16LB A-106B 0.2580 7.504 0.598 8.101' CS16-DB-01-1038 16i A-106B- 1.0310 3.001 0.598 10.798 CS-16-DB01-1045 16 I A-106 B .l.0310 3.001 0.478 10.439 CS16-DB-01-1103 16 E A-106 B 1.0310 3.001 0.598 10.798 CS16DB-011104 16 W A-106B 1.0310 1.501 0.897 7.192 CS20-DB-01-1115 20 fB A-106B 1.2800 4.410 0.594 15.012 CS04-DB021232 ( LB A106B 0.3370 8.149 0.499 8.649 CS04-DB-021233 4W 'A-106B 0.3370 1.630 0.749 2.379 BS-24-IB-01-1012 0 SP 0.0000 0.000 0.000 0.000 HS-24IB-011101 24 W A 106 B . 0.8680 0.035 1.057 3.275 MS-24EB-01-1102 24LB A 106 B 0.8680 0.173 0.705 2.634 MS30IB-01-1220 30 LB A-155(C70 0.9080 0.111 0.611 2.347 HS-30-IB01-122t 30W A-1551070 0.9080 0.022 1.007 3.088 HS-30 !S-01-13'.J 30 fB A-155IC70 0.9080 0.089 0.671 2.280 55-188802-1001 18 0 A-106B 0.7500 0.000 1.173 1.173

-BS-24-IB021001 24LB A-106B 0.8680 0.000 1.068 1.068

-BS24-IB-021303 24W A-106 B 0.8680 US0 2.0 0 . 2.002 MS24-IB-021004 2(t A-106 B 0.8680 J0 1.335 1.335 MS 06-IB 02 1006 6E A-106B 0.2800 0.000 1.854 1.854 MS 06-IB-0(-1123 6W A-106B 0.2800 0.019 0.927 2.837 FD-08-IB061401 8W A106B 0.4060 0.011 1.565 -4.726 FD-06IB061419 i fB A-106B 0.2800 0.113 1.236 4.047  ;

TD-06IB06-1421 JW A-106B 0.2800 0.028 1.854 5.645 FD-06-IB-06-1430 6I A-106 B 0.2800 0.057 1.236 1.292 CS-IS-IB09-1002 16i A-106B 0.8430 1.451 0.101 8.458 l 0506-18-09-1002 6I A 106 B 0.4320 1.032 0.556 3.175 ]

CS06IB-091003 6W A106B 0.4320 0.516 0.833 2.699 CS-16IB-091905 16I A-106B 0.8430 1.451 0.561 6.037 CS 16-IB 09 1008 16LJ A-106B 0.8430 0.726 0.561 3.860 CS16IB-09-1923 16 W A-106B 0.8430 0.484 1.052 4.607 CS-16IB-09-1024 16 W A-106 B 0.8430 0.484 1.052 4.607 CS 16-EB-09 1032 16 i A-106B 0.8430 1.724 0.408 6.395 )

CS 16-IB-09-1035 16I A-106B 0.8430 1.724 0.510 6.701 1 I

'CS 16-IB-09 1043 16 SRI 4-106 B 0.8430 2.011 0.408 7.257 CS16-IB-09-1059 16 i A106B 0.8430 1.724 0.408 6.395 CS-16 IB-09-1061 16LJ A-106B 0.8430 0.882 0.399 3.783 CS 16-IB 09 !!01 16 W A-106 B 0.8430 0.726 1.052 5.333 CS16-IB-091102 16E A-106B 0.8430 1.451 0.701 6.458 j CS 06-IB 09-1102' 6I A-106 B 0.4320 1.032 0.444 2.953 l CS 16 IB 09 1103 16 W A106B 0.8430 0.726 1.052 5.333

{Page No. *' 3 i;4t/26/81

,IIAHPOINTCHal&CfillSTICS .

IIAH ?0117 ' ~D IAuffit C0lflG. BattilAL AStu t-C STitSS OitRALL (II.) N0HIIAL BADIESS BADNESS EADNESS WALL FA070R TA0701 FAC70H (II.)

CS16-EB-09-1105 '16l' A 106 B 0.8430 1.451 0.561 6.037 C5-1688-09!!08 16LJ A-106B 0.8430 0.726 0.561 3.860

.CS-16-EB-09-1111 16I A 106 B 0.8430 1.451 0.561 6.037 CS16IB-091113 =16 W A-106B. 0.8430 0.726 1.052 5.333

~C516-88-091130 16I A 106 B 0.8430 1.724 0.412 6.408'

.CS-16-tB091133 16 I A106B- 0.8430 1.724 0.515 6.717 CS 16-!B-091152 16SEI A-106 B 0.8430 3.017 0.515 10.596 i

.CS-16IB091161. 16 I .A 106 B 0.8430 1.724 0.515 6.717 CS 16-IB 09 1182 16 I A-106 B- 0.8430 1.149 0.412 4.684 CS16IB091186 .16I A-106 8 0.8430 1.724 0.412 6.408 CS16-IB-091188 16LJ A-106 B. 0.8430 0.862 0.399 3.783

-FD-10-GB-021003 10W A106B 0.3650 4.578 0.463 15.125 F3-10GB-02-1021 '

10Bf A 106 B. 1.4400 22.891 0.309 69.601

' FD 10-GB-021108 10fJ A106B 0.5930 4.578 0.220 14.395 TD10-GB021116 10LB A 106 8 0.5930 22.891 0.176 69.203 FD 10 GB-021120 - 10Bf- A-106 B' 1.4400' 22.891 0.309 69.601 FD12GB-031005 12SRt A-106B 0.3750 6.338 0.344 20.046 F310-GB-031007 10I 'A-106B 0.3650 2.608 0.370 8.933 lfD-10GB03-1009 -10 W A 106 B 0.3650 1.304 0.555 5.575 1D-1208-031009 12W A-106 B 0.3750 1.811 0.515 6.979 F312Gi-031016 12 W A 106 B 0.3750 1.811 0.644 7.366 TD12GB03-1017 12i A-106 B 0.375u 3.622 0.429 12.154 ,

CS-10-GB04-1000 18 0.3750 0.000 0.000 0.000 CS 18 GB-04 1001 18fII A-106 B 0.3750 7.905 0.417 24.966

~08-12-G8041005 12I A-106 B 0.3750 3.525 0.278 11.408 CS20-GB041007 20 Sit A-106 B 0.U50 6.723 0.371 21.281 C5-20-0B04-1008 20 W A-106 B 0.3750 1.921 0.556 7.430 CS-10-GB04-1010 16 Sit A 106 B 0.3750 4.150 0.417 13.701 C5 12 08-04 1913 12 i A-106 B 0.3750 3.525 0.278 11.408

.CS-10-GB041914 18 Sit A-106 B 0.3750 2.767 0.333 9.301 CS20Gb-04-1019 20 W A106B 0.3750 1.921 0.695 7.847 CS-18GB-041113 18 W A106B 0.3750 0.674 0.668 4.026 C5 12-G3-04-1123 12 I A-106B 0.3750 2.275 0.297 7.715 CS-12-GB041211 12LB A-1068 0.3750 7.583 0.230 23.437 f3-03-GB05ll26 8 LB A-106B 0.3220 0.000 0.000 0.000 l TD-08-GB-05-!!!8 8 Sit A-106 B 0.3220 3.521 0.377 11.694 TD-08CB-05-1214 8SBI A-106 B 0.3220 3.521 0.3'7 11.694 FD-08GB-051231 8 LB A 106 B 0.3220 5.030 0.377 16.221 FD08CB-05-!!33 8 SRI A-106 B 0.3220 3.521 0.377 11.694 CS-18-GB-07-1010 18W A-!OS B 0.3750 1.186 0.568 ' 5.263 CS18-GB-0710!! 18 SRI A 106 B 0.3750 4.150 0.379 13.587 05-18-G8-071016 18LB A 106 B 0.3750 5.929 0.379 18.923 CS-18CB071017 16 W A-106 B p.3750 1.186 0.568 5.263 CS 18 GB-07 1022 18 SRI A-106B 0.3750 4.150 0.3 0 13.587 CS-18-GB071036 18 SRI A 106 B 0.3750 4.150 0.379 13.587 CS 10 GB 07 1041 18LB A-106B 0.3750 5.929 0.379 18.923 CS 18-CB 07 1042 18 W A-106 B 0.3750 0.000 0.568 7.705 l:

L

x, lj I

inte50.4: 3

.s:06/26/81 IIAHPOINTCBARACTIllSflCS.

IIAHPO!Ifi .DIAltttiColflG.HAftt!AL ASTE .E-C 57BISS OVEHALL-(II.) 10HilALBADitSSBADIESSBADHISS l WALL FACTOR FACTOR FAC70B (II.)

8S12G001-!!31- 12 W- A-312 SS304 0.3750 -0.000 0.994 2.983 i US-12-GD01ll32 12I A 312 SS304 0.3750 0.000 0.663 1.989 HS 12-GD 01-ll33 12W A-312 SS304 0.3750 0.000 0.994 2.983 US-12-GD-01-1134 12W A-312 S$300 0.3750 0.000 0.994 2.983-BS-12-CD-011135- . 12 I . A-312 SS304 0.3750 0.000 0.663 1.989 HS-12CD-01-1136 12W A-312SS304.0.3750 0.000 0.796 2.387 H312GD-01-1250 12W A-312 S$304 0.3750 0.000 0.994 2.983 HS12-CD011251 12i A-312 SS304 0.3750 0.000 0.663 1.989

- MS 12-GD-01-1252 12 W A-312 S$304 0.3750 0.000 0.994 2.983 FD 034B 011119 8 fB A-106B 0.3220 1.903 0. d8 6.061 FD08-HB-01-1120 !W A-106B 0.3220 0.000 0.176 0.529 TD-0843-01-1121 - 8W A-106B -0.3220 0.3 17 0.176 1.481 FD18-HB0210lf 16 W A106B 0.3750 0.690 0.328 3.056 FD-164B 02-1018 16 SRI A 106 B 0.3750 2.4 16 0.219 7.905 FD 104B-03-1112 10LB A-106B 0.3650 3.219 0.405 10.871 10-10 4 8-03 1212 .10LB A-106 B- 0.3650 3.219 0.405 10.871 FD08-8B-041001 8W A 106 B 0.3220 0.052 0.192 0.733

' FD4848 041002 '8W A 106 B 0.3220 0.052 0.154 0.618

. FD-084D-04-1003 8 SHI A 106 B 0.3220 0.183 0.102 0.856

-FD-08-HB-041004 8W A-106B 0.3220 0.052 0.154 0.618

. FD 124B-04-1005 12i A-106B 0.3750 0.073 0.106 0.536 iD-1248-041012 , !! W A-106B 0.3750 0.088 0.158 0.738 FD 1248 041013 - 12I A-106 8 0.3750 0.175 0.106 0.842 FD-124B-041014 12W A-106 B 0.3750 0.088 0.158 0.738 TD-08-HB051004 8LB A 106 B 0.3220 0.000 0.015- 0.045 FD-06-HB-05-1068 60 A-106 B 0.2700 0.000 0.013 0.040 HS-12HB07-1001 0 0.0000 0.000 0.000 0.000 FD-12EB-181001 12W A-106B 0.3760 (3.790 0.198 43.988 FD-14-BB-18-1001 14 W A-106B 0.3750'14.434 D.231 43.994

' TD 124B-181002 12W A 106 B 0.3750 29.193 U.158 29.352 FD-144B-181002 14 W A-106 B 0.3750 14.434 0.231 43.994 TD-124B-18-1003 12I A-106B 0.3750 58.386 0.106 58.492 FD-14-HB-18-1005 14i A106B 0.3750 28.867. 0.123 86.972 l ID-124B 18-1006 12I A106B 0.3750 87.579 0.106 87.685 I FD 144B-181008 14SP A-106 B 0.3750 2,887 0.123 9.030 )

7D-1448-18 1009 14LB A-312 SS304 0.3750 0.000 0.195 0.585 FD-1248-18-1011 12i A-108B 0.3750 87.579 0.106 87.685 FD-144B 181014 14 t A-106B 0.3750 28.867 0.123 88.972 FD-124B-18-1014 12i A-105B 0.3750 67.579 0.106 87.685 ,

TD-1248-18 1017 12I A-106 B 0.3750 87 59 0.106 87.685 )

FD 1248-181022 12LB A-106 B 0.3750145.970 0.106 146.071 l TD-1(4B-181023 141 A 106 B 0.3750 28.867 0.123 86.972 TD-1248-18 102( 12i A106B 0.3750 87.579 0.106 87.685 FD12-EB-181029 12I A 106 B 0.3750 17.579 0.106 67.685 H5184D-041123 18 0 A 106 B 0.3750 5.134 0.255 16.166 HS 184D-041127 18 0 A 106 B 0.3750 5.131 0.20( 16.013 HS-184D-04-1204 18 W A 312 SS304 0.3750 0.000 0.485 1.454

o Page No.

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~

t08/26/87

\

!!AHP0lltCHAHACTIBISf!CS t-C Sff!SS OilBALL IIAHP0llt DIAMitt!001 FIG.HAftBIAL ASTE "

(II) N0HINA:,BADNISSBADNISSBADNESS -

WALL FACTOR FACTOR FACTOR j (II.)

)[

MS-18HD-04-1206 18 W A-312 SS304 0.3750 0.000 0.485 1.454 95-18HD-04-1228 180 A-106 B 0.3750 5.134 0.255 16.166 l 95 18 ED-04-1241 18 W A-312 SS304 0.3750 0.000 0.485 1.454 k l RS-03-SA-60-1166 3I A 312 SS304 0.2160 0.000 1.419 4.256 i IS03-SA-60-1167 3W A 312 SS304 0.2160 0.000 2.128 6.385 RS-03SA-60-Il69 3W A 312 SS304 0.2160 0.000 2.128 6.385 i

RS-03 SA-60-1170 30 A-312 SS304 0.7160 0.000 1.419 4.256 RS-03-$1-60-1171 3W A-312 S$304 0.2160 0.000 2.128 6.385 BS-03 SA-60-1175 3W A-312SS30( 0.2160 0.000 2.128 6.385 RS-03SA60-!!78 3I A-312 SS304 0.2160 0.000 1.419 4.256 RS-03-SA60-1179 3W A-312 SS304 0.2160 0.000 2.128 6.385 RS-03-SA-60-1180 3W A-312 SS304 0.2160 0.000 1.703 5.108 .

GS-36-II 01 1102 36i A 53 9 0.5000 13.958 0.295 42.762 MS-29-II01-1104 29LB A-53 B 0.5000 53.776 0.238162.041 H5-291101-1105 29LB A-53 B 0.5000 53.776 0.238162.0(1 HS-40-II-011106 40LRt A-53B 0.5000 16.960 0.328 51.863 H329-11-01-!!06 29 LB A 53 B 0.5000 53.776 0.238162.041 MS36-II-01-1108 36i A-53B 0.5000 13.958 0.295 (2.762 US40II-011108 40LB A-53B 0.5000 56.532 0.328170.580 HS-40-II-01-1110 40LHI A 53 B 0.5000 16.960 0.328 51.863 GS29-II-011110 29I A53B 0.5000 21.510 0.238 65.245 GS-40-II-01-1117 40LB A 53 B 0.5000 56.532 0.328 170.580 HS40II011118 40 W A-53B 0.5000 11.306 0.492 35.396 DS 40-II 01-1119 40 0 A-53 B 0.5000 11.306 0.328 34.904 95-29-1101-1125 29LJ A 53 B 0.5000 10.755 0.238 32.979 95-291101-1126 29LB A53B 0.5000 53.776 0.238 162.041 "

US-40-II-01-1201 40 0 A 53 B 0.5200 11.306 0.328 34.904 0529-110!-1201 29W A538 0.5000 10.755 0.4(6 33.60(

G529-11-01-1202 29W A 53 B 0.5000 10.755 0.446 33.604 US-36II-011205 36LB A-53 B 0.5000 34.896 0.295105.575 US-36II011206 36LB A 53 8 0.5000 34.8S6 0.295105.575 US-40-II01-1207 40 LB A 53 B 0.5000 56.532 0.328 170.580 GS-40-II-01-1209 40I A-53 B 0.5000 22.613 0.328 68.823 05-291101-1209 29I A 53 B 0.5000 21.510 0.238 65.245 HS-40-II-01-1209 40I A-538 0.5000 0.000 0.000 0.000 ,

25 40 11-01-1211 40 W A-53B 0.5000 !!.306 0.492 35.396 GS-36II01-1212 %W A-53 B 0.5000 6.973 0.554 22.600 GS 29-II-01-1217 29LB A-53 B 0.5000 53.776 0.238162.041 HS 29-II-01-1218 29LB A-53 B D.5000 53.776 0.233162.041 932911-011222 29LB A-53B 0.5000 53.776 0.238162.041 1

I

7 1

ATTACHMENT'

.. IEB 87-01 RESPONSE H: SECTION B-TABLE B-4 LINE DESCRIPTION,

' E*X .

MS, - ' EB-01 ..- XXXX Unique Point Identifier

~ Line Class As Per Attached Table System-MS Main Steam

CS Condensate FD Main Feed RS Radwaste Steam i

l

TABLE B-4 Page 1 l

l PIPING CLASS

SUMMARY

, j l

DESIGN SERVICE CONDITION RATING NORMAL MAXIMUM INSUL .

d CLA'l5,, SERVICE PSIG 2 PFIG ' F, PSIG 2 CLASS DB-1 Boiler Feedwater Pumps to Containment Isolation Valve 1525 436 1042 437 II DB-2 Boiler Feedwater Pumps Recircula-tion to condenser Block Valves 1525 436 1042 350 III Emergency Feedwater Pumps to j DB-3 Containment Isolation Valve & t Recirc Piping 1440 100 1190 100 DB-4 Heater 51-58 Vents & Drains (Channel Side) 1525 436 1042 436 II EB-1 Main Steam Supply to Turbine 1085 555 775 517 II EB-2 Turbine Bypass Steam to Condenser Block Valves 1085 555 765 515 II EB-3 Main Steam to Turbine Accessory Systems Reducing Stations & to ,

Air Ejectors 1085 555 765 515 II i EB-4 Main Steam to Rtrheaters 1085 555 775 517 II EB-5 Main Steam Line Vents & !> rains 1085 555 775 517 II EB-6 Reheater Drains & Vents (through Control Valve Assemblies) 108!, 555 755 514 II EB-7 Blowdown Lines (to Blowdown Tank Control Valves) 10R5 555 755 517 II i EB-8 Main Steam to Auxiliary Feedwater Pump Turbine 1085 555 765 515 I:

EB-9 Boiler Feedwater from Contain-ment Isolation Valves to Steam Generators 1310 436 900 436 II

{

ES-10 Emergency Fee & M n from contain-ment Isolation valves to Main Feedwater Line 1310 100 900 100 1310 100

=-_____-__.___-______

TABLE B-4 Page 2 I

l DESIGN SERVICE CONDITION ETING NORMAL MAXINUM . INST /L CLASS SERVICE PSIG ' F, ' PFIG 'F PSIG 2 CLASS EB-11 . Nitrogen Supply to Containment Area Downstream of Control Valve 900 105 900 105 EB-12 Steam Generator. Blowdown Line from the Blowdown Tank Control Valves to HX-18', From HX-18 to the First "0FF" Isolation valves 1085 555 755 517 II EB-13 Miscellaneous Drains to condenser 150 500 .,

' GB Branching Vents, Dumps and Drains From Extraction Steam to 5A'& 58 Feedwater Heaters 370 441 394 441 II GB-2 Reheater Drains to Heaters '

SA 5B Downstream to Control Valves 370 51) 374 515 I::

GB-3 Heaters Drain Pusp Discharge 517 352 340. 352 III GB-4 Condensate Pusp Discharge to j Feedwater Pusp Suction ---

Through Heater 2 400 95 ,

Heater 2 to Heater 3 400 211 IV I Heater 3 to Heater 4 400 267 III J Heater 4 to Feed Pusy Suction 400 348 III Valves (MS-50, MS-51)

GB-5 Heaters 5&-58 Drains to Heaters 4&-48 (Upstream of ,

i Control Valves) & D g to  !

Condenser throuq$1 Control Valve Assemblies 370 361 370 361 III Condensate Discharge to & from j GB-6 Feedwater Pump Seals 400 100 350 88 '

GB-7 Velves MS-50-& MS-51 to Feed Pusy 415 348 i

GB-8 From HK-18 Shellside Discharge 400 285 345 to First "0FF" Isolation Valve 1 GD-1 HP Turbine Extraction To SA & 58 300 850 Feedwater Heaters l

-.___.__m.__ _ _ _ _ _ . _ _

TABLE B-4

  • Page 3 DESIGN SERVICE CONDITION RATING NORMAL MAXIMUM INSUL CLASS SERVICB PSIG 'F PFIG ' F, PSIG 'F CLASS HB-1 Moisture Separator Drains to Drain Tank & Dumps through Control Valve Assemblies to Condenser 150 355 129 355 III HB-2 Heaters 4A-48 Drains to Drain Tank 150 355 129 355 III HB-3 Heaters SA-58 Drains to Heaters 4A-48 (Downstream of Control Valves) 150 361 129 361 III HB-4 LP Extraction Steam to Heaters 4A-48, Vents, Dumps & Drains 150 355 125 352 III HB-5 Heaters 3A-35 Vents, Dumps &

Drains 50 272 26 272 III

,HB-6 Heaters 1A-18, 21-28, Vents, 40 240 1.44 216 IV l Dumps & Drains vac vac ,

HB-7 LP Auxiliary Steam 50 300 30 275 III HB-8 Cooling Water (Condensate to Miscellaneous Pusps 400 100 10-15 90

.HB-9 Blewdown Tank Discharge, ata Vents & Drains 50 212 Vtr HB-11 Gland Steam Relief Valve Stack 163-

& Heaters Relief Valves 1-2 40 216 IV Discharge 3 50 272 III 4-5 150 361 III HB-12 Turbine Bypass Downstream of Condenser Block Valves 50 281 III l

HB-13 Miscellacious Drains to Condenser 150 503 IVp HB-14 Drains & Vents from Air Ejector Inter & After Cooler, Gland Seal Condenser & Hogger 50 250 IVp HB-15 Emergency Feed Pump Turbine Exhaust 10 240 IVp

TABLE B-4 Page 4 DESIGN SERVICE CONDITION.

RATING NORMAL MAXIMUN INSUL CLASS SERVICE PSIG 3. PFIG 2 PSIG 'F, CLASS HB-16 Miscellaneous Stamp Vents to

. Atmosphere & Freon Relief Vunt atn 212 IVp HB-17 Condensate Pumps & Condensate

, Transfer Pumps' Suction, Drains &

Vents- 20 100 vac 89 HB-18. Heaters Drain Pump Suction, & P mp '

through control Valve Assemblies to Condenser, Vents &' Drains 129 355 122 '352 III HB-19 Service Water to Engineered Safeguard Equipment 100 100 75 70 Vias HB-20 Water to. Fish. Rearing Facilities HB-21 Condenser Evacuation Ata-&

Piping Full Vac. 100 ,

HB-22 Diesel Fuel 011 100 100 50-80 100 HB-23 Lube oil- 85 100 25 100 HB-24 Nitrogen Gas - Low Pressure 175 100 150 100 HB-25 Hydrogen & Carbon Dioside Gas 100 100 100 100 HB-26 Heater Drain Tank Pump Recircu-lation Downstrees of Shutoff Va!.ve 129 355 122 352 III HB-27 Drains to Condenser, Downstream to control Valve' Assemblies 50 500 IVp i

HB-28 Condensate Transfer Pump Discharge 100 100 HB-29 Diesel Enhaust atm 1000 atm 1000 In As per HB-30 Condensate Returns 150 500 Primary Source HB-31 Lube Oil & Fuel Oil Vapor Vents ata 100

TABLE B-4 Page 5 3

DESIGN SERVICE CONDITION RATING NORMAL MAXINUM INSUL CLASS SERVICE PSIG ' F, PFIG ' F, PSIG 'F CLASS HB-32' Miscellaneous Drains atm 100

'HB-33 SG Blowdown from HX Discharge 150 560 Isolation Valve to Blowdown Tank HB-34 '- Blowdown Tank Bypass Line.from 150 500 i HX Discharge Isolation Valve Through Blowdown Filters to SW Return Isolation Valve

-HB-35 HX-18 Relief to SG Blowdown 150 500 Return Line HD-1 Main Header for Drains; Dumps to Condenser 50 550 50 517 II l

HD-2 Blowdown to Blowdown Tank Down-stream of Blowdown valves 50 550 50 517 II HD-3 Throttle & HP Trap Drains to Condenser HD-4 Extraction to 4Ada Feedwater -

Heater Isolation Valves 150 355 125 352 III JB-1 Service Water (Outside of Area of Engineered Safeguards Equipment) 100 100 75 100 VIan JB-2 Service Water Returns from Safeguards Equipment -

Heating Boiler Blowdown 50 300 IIIp JB-3 l JB-4 Component Cooling Water (Outside l

of Area of Engineered Safeguards Equipment) 100 100 75 100 JB-5 Caustic 115 150 85 130 JB-6 Condenser Waterbox Vents & Drains 25 100 l

Chilled Water 100 40 Vias JB-7

4 TABLE B-4 Page 6 I

DESIGN SERVICE CONDITION RATING NORMAL MAXINUM INSUL ,

CLASS SERVICE PSIG 'F PFIG 'F PSIG 'F CLASS j l

J' 8 JB- 9 Neutralizing Tank Effluent 15 150 JB-10 Clarifier Sludge t1 Plant Effluent Sump 50 100 JB-11 Miscellaneous Vents & Drains atm 100 JB-12 Plant Meating Steam 50 300 30 275 III JB-13 Plant Heating System Condensate Returns 50 300 30 275 III JB-14 Process Steam 50 300 30 275 II JB-15 Heating Boiler Feed Pump Suction & Discharge 100 100 50 100 JB-16 Miscellaneous Sump Pump Discharge i

JD-1 Potable Water 100 100 60 75 80 75  ;

JD-2 Hot Water Heating 20 200 15 200 IV JF-1 Circulating Water to Condensers and condannate Coolers 25 100 15 100 JG-1 Domineralizar Water to Monitor Tank 125 100 95 100 JG-2 Condensate Reject & Makeup 50 100 JG-3 Demineralized Water to Storage 125 100 95 100

TABLE B-4

,4 Page 7 1'

' DESIGN SERVICE CONDITION RATING NORMAL MAXTWM IllSUL CLASS SERVICE PSIG 3 PFIG 2 P,SJ ] , CLASS JG-4 Auxiliary Feedwater Pump Suction from Condensate Tank & Auxiliary Feedwater Pump Recirc Downstream of Control Valve 50 100 15 100 JG-5 Controlled Lab Drains atm 150 IV JG-6 Misc. Drains & Vents (Non-radioactive) ata 150 IV JG-7 Containment Air Sample JG-8 Liquid Wate (Radioactive) Embedded

. Drains from El. 19'-3" & 5' to Building Suq & Monitor Drains

_JG-9 Air Sparging Line to Neutralizer q Tank 100 100 ,

JG-10 Chemical Drains (Radioactive)

JG-11 Demineralized Water to Phosphate, Hydrazine & Morpholine Inj Tanks 125 100 95 100 JG-12 overflow from chemical Injection Tanks JG-13 Heating Boiler Feed Pump Suction i KB-1 Fire Servica Water (Above Ground) 125 100 i

KC-1 Fire Servica Water (Below Ground) 125 100 KC-2 Misc Sump Discharge Lines ,

(Below Ground)

KC-3 Portable Water Supply 100 80 ,

L

TABLE B-4 Page S j

i SERVICE CONDITION i DESIGN RATING NORMAL- MAXIMUM INSUL CLASS SERVICE PSIG 2 PFIG 'F PSIG 2 CLA_SS LB-1 Non-contaminated Drains & Vents (Buried or Embedded) i i

LC-1 Building & Sanitary Drains (Outside of Building)

LD-1_ Roof Floor & Equipment Drains (Suspended) 1 LE-1 Sanitary soil Waste.& Vents (Suspended) ,

MC-1 Acid Drains (Suspended and Embedded)

MD-1 Contaminated Equipment & Floor Drains (Corrosives) l MD-2 Ventilation Piping, ME-1 Ch eical Feed to Steam Generator Piping 1310 100 ME-2 Chemical Feed to Steam Generator Tubing 1310 100 ME-3 Misc Sampling Systems Var Var

( .

l

g- y - _ _

TABLE B-4 Page 9 DESIGN SERVICE CONDITION RATING NORMAL MAXIMUM' INSUL CLASS SERVIC3 PSIG *F PRIG *F PSIG *F CLASS I

MF-1 Chemical Feed To Condensate System - Piping 500 100 MF-2 Chemical Feed To Condensate System - . Tubing 500 100

?

MR-1 Contaminated Equipment & Floor Drains & Plumbing Systems (Non-Corrosive. .

>1 NS-1 Instrument Air Downstream of Dryer 125 100 125 100 l

I 1 Service Air & Instrument Air Upstream of Dryer 125 100 125 100 08-2 Diesel Generator Starting Air 250 100 250 100 PB-1 Chemical Flush Ata 100 l

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